EP1787977A4 - Process for producing high-purity diphenyl carbonate on commercial scale - Google Patents

Process for producing high-purity diphenyl carbonate on commercial scale

Info

Publication number
EP1787977A4
EP1787977A4 EP05777109A EP05777109A EP1787977A4 EP 1787977 A4 EP1787977 A4 EP 1787977A4 EP 05777109 A EP05777109 A EP 05777109A EP 05777109 A EP05777109 A EP 05777109A EP 1787977 A4 EP1787977 A4 EP 1787977A4
Authority
EP
European Patent Office
Prior art keywords
diphenyl carbonate
commercial scale
reaction mixture
quality
production process
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP05777109A
Other languages
German (de)
French (fr)
Japanese (ja)
Other versions
EP1787977A1 (en
Inventor
Shinsuke Fukuoka
Hironori Miyaji
Hiroshi Hachiya
Kazuhiko Matsuzaki
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Asahi Kasei Chemicals Corp
Original Assignee
Asahi Kasei Chemicals Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Asahi Kasei Chemicals Corp filed Critical Asahi Kasei Chemicals Corp
Publication of EP1787977A1 publication Critical patent/EP1787977A1/en
Publication of EP1787977A4 publication Critical patent/EP1787977A4/en
Withdrawn legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14Fractional distillation or use of a fractionation or rectification column
    • B01D3/143Fractional distillation or use of a fractionation or rectification column by two or more of a fractionation, separation or rectification step
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C68/00Preparation of esters of carbonic or haloformic acids
    • C07C68/08Purification; Separation; Stabilisation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14Fractional distillation or use of a fractionation or rectification column
    • B01D3/16Fractionating columns in which vapour bubbles through liquid
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07BGENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
    • C07B61/00Other general methods
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C68/00Preparation of esters of carbonic or haloformic acids
    • C07C68/06Preparation of esters of carbonic or haloformic acids from organic carbonates
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C69/00Esters of carboxylic acids; Esters of carbonic or haloformic acids
    • C07C69/96Esters of carbonic or haloformic acids
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency

Abstract

This invention provides a production process of diphenyl carbonate which can produce high-purity diphenyl carbonate usable as a starting material of a high-quality and high-performance polycarbonate from a reaction mixture composed of a catalyst and a reaction by-product obtained, for example, from a transesterification using a dialkylcarbonate and phenol as a starting compound, on a commercial scale of 1 ton/hr stably for a long period of time. Although there are many proposals on a production process of a reaction mixture containing aromatic carbonates, for example, by reaction distillation, all of them are for a small, short-term and experimental scale. Accordingly, any specific method or apparatus, which can mass-produce, from the reaction mixture, a high-purity diphenyl carbonate usable as a starting compound for a high-quality, high-performance polycarbonate on a commercial scale have not hitherto been disclosed. In the production process of the present invention, a high-boiling substance separation column (A) comprising two specific continuous multistage distillation columns and a diphenyl carbonate purification column (B), are provided. When an apparatus comprising these columns connected to each other is used, a high-purity diphenyl carbonate important as a starting compound for a high-quality and high-performance polycarbonate can be produced stably from a diphenyl carbonate-containing reaction mixture on a commercial scale of at least 1 ton/hr for a longer period of time.
EP05777109A 2004-09-02 2005-08-31 Process for producing high-purity diphenyl carbonate on commercial scale Withdrawn EP1787977A4 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2004255379 2004-09-02
PCT/JP2005/015853 WO2006025424A1 (en) 2004-09-02 2005-08-31 Process for producing high-purity diphenyl carbonate on commercial scale

Publications (2)

Publication Number Publication Date
EP1787977A1 EP1787977A1 (en) 2007-05-23
EP1787977A4 true EP1787977A4 (en) 2008-08-06

Family

ID=36000074

Family Applications (1)

Application Number Title Priority Date Filing Date
EP05777109A Withdrawn EP1787977A4 (en) 2004-09-02 2005-08-31 Process for producing high-purity diphenyl carbonate on commercial scale

Country Status (8)

Country Link
US (1) US20070260083A1 (en)
EP (1) EP1787977A4 (en)
JP (1) JP4236205B2 (en)
KR (1) KR100879497B1 (en)
CN (1) CN101010284B (en)
BR (1) BRPI0514732A (en)
EA (1) EA200700530A1 (en)
WO (1) WO2006025424A1 (en)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006001257A1 (en) * 2004-06-25 2006-01-05 Asahi Kasei Chemicals Corporation Process for producing aromatic carbonate on commercial scale
CN100532347C (en) 2004-07-13 2009-08-26 旭化成化学株式会社 Industrial process for producing aromatic carbonate
WO2006022294A1 (en) 2004-08-25 2006-03-02 Asahi Kasei Chemicals Corporation Process for producing high-purity diphenyl carbonate on commercial scale
BRPI0514693A (en) * 2004-09-03 2008-06-17 Asahi Kasei Chemicals Corp improvement in an industrial process for the production of high purity diaryl carbonate, high purity diphenyl carbonate, and apparatus for producing the same
EP1801095B1 (en) * 2004-10-14 2012-07-18 Asahi Kasei Chemicals Corporation Process for production of high-purity diaryl carbonate
EP2121563B1 (en) * 2007-02-16 2016-05-04 SABIC Global Technologies B.V. Process for manufacturing dimethyl carbonate
US7799940B2 (en) * 2007-02-16 2010-09-21 Sabic Innovative Plastics Ip B.V. Process for manufacturing dimethyl carbonate
DE102007055266A1 (en) 2007-11-20 2009-05-28 Bayer Materialscience Ag Process for the purification of diaryl carbonates
KR101411016B1 (en) * 2011-12-27 2014-06-23 제일모직주식회사 Catalyst, method for preparing the same amd method for preparing aromatic carbonate from dialkyl carbonate using the catalyst
WO2023068288A1 (en) * 2021-10-21 2023-04-27 旭化成株式会社 Method for producing diphenyl carbonate

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1783112A1 (en) * 2004-08-25 2007-05-09 Asahi Kasei Chemicals Corporation Industrial process for production of high-purity diphenyl carbonate

Family Cites Families (20)

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Publication number Priority date Publication date Assignee Title
US4182726A (en) * 1974-06-25 1980-01-08 Snamprogetti, S.P.A. Process for the preparation of aromatic carbonates
IT1025961B (en) * 1974-11-25 1978-08-30 Snam Progetti PROCESS FOR THE PREPARATION OF AROMATIC CARBONATES
DE2736063A1 (en) * 1977-08-10 1979-02-22 Bayer Ag Process for the preparation of aromatic carbonic acid esters
US4410464A (en) * 1982-03-15 1983-10-18 General Electric Company Diaryl carbonate process
CA1219187A (en) * 1983-11-22 1987-03-17 Marc-Andre Poirier Process for breaking emulsions produced during recovery of bitumens and heavy oils
US4552704A (en) * 1983-12-27 1985-11-12 General Electric Company Process for the production of aromatic carbonates
US4554110A (en) * 1983-12-27 1985-11-19 General Electric Company Process for the preparation of aromatic carbonates
CA2041646C (en) * 1989-12-28 1999-06-15 Shinsuke Fukuoka Process for continuously producing an aromatic carbonate
JP3033062B2 (en) * 1990-08-21 2000-04-17 旭化成工業株式会社 Manufacturing method of aromatic polycarbonate
WO1992009357A1 (en) * 1990-11-29 1992-06-11 Nitto Denko Corporation Liquid-filtering film and filtering device using said film
JPH0791234B2 (en) * 1990-12-26 1995-10-04 旭化成工業株式会社 Continuous production of aromatic carbonates
DE4218061A1 (en) * 1992-06-01 1993-12-02 Bayer Ag Process for the production of organic carbonates with at least one aromatic ester group
DE4226756A1 (en) * 1992-08-13 1994-02-17 Bayer Ag Process for the production of dicarbonates
DE4226755A1 (en) * 1992-08-13 1994-02-17 Bayer Ag Process for the continuous production of diaryl carbonates from dialkyl carbonates
JP3865420B2 (en) * 1995-10-17 2007-01-10 三菱化学株式会社 Diaryl carbonate production method
IT1282363B1 (en) * 1996-01-16 1998-03-20 Enichem Spa CONTINUOUS PROCEDURE FOR THE PREPARATION OF FENYL METHYL CARBONATE
SG52906A1 (en) * 1996-01-17 1998-09-28 Asahi Chemical Ind Method for producing an aromatic polycarbonate having improved melt stability
JP4112048B2 (en) * 1997-09-16 2008-07-02 旭化成ケミカルズ株式会社 Process for producing aromatic carbonates
US6600061B1 (en) 2000-11-15 2003-07-29 General Electric Company Method for the continuous production of aromatic carbonates
AU2003206228A1 (en) * 2002-02-05 2003-09-02 Lg Chem, Ltd. Continuous method for preparing aromatic carbonate using a heterogeneous catalyst and a reaction apparatus for the same

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1783112A1 (en) * 2004-08-25 2007-05-09 Asahi Kasei Chemicals Corporation Industrial process for production of high-purity diphenyl carbonate

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of WO2006025424A1 *

Also Published As

Publication number Publication date
EA200700530A1 (en) 2007-08-31
JP4236205B2 (en) 2009-03-11
CN101010284B (en) 2011-06-22
EP1787977A1 (en) 2007-05-23
KR100879497B1 (en) 2009-01-20
WO2006025424A1 (en) 2006-03-09
BRPI0514732A (en) 2008-06-24
US20070260083A1 (en) 2007-11-08
KR20070039975A (en) 2007-04-13
JPWO2006025424A1 (en) 2008-05-08
CN101010284A (en) 2007-08-01

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